NO20054297L - Automatisk krakkingsreaktor - Google Patents

Automatisk krakkingsreaktor

Info

Publication number
NO20054297L
NO20054297L NO20054297A NO20054297A NO20054297L NO 20054297 L NO20054297 L NO 20054297L NO 20054297 A NO20054297 A NO 20054297A NO 20054297 A NO20054297 A NO 20054297A NO 20054297 L NO20054297 L NO 20054297L
Authority
NO
Norway
Prior art keywords
gaseous
gaseous reactant
zone
delivery
delivery device
Prior art date
Application number
NO20054297A
Other languages
English (en)
Inventor
Derek Alan Colman
Ian Allan Beattie Reid
William Terence Woodfin
Michael John Alexan Matthewman
Vaughan Clifford Williams
Original Assignee
Bp Chem Int Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Priority claimed from GB0303723A external-priority patent/GB0303723D0/en
Priority claimed from GB0329710A external-priority patent/GB0329710D0/en
Application filed by Bp Chem Int Ltd filed Critical Bp Chem Int Ltd
Publication of NO20054297L publication Critical patent/NO20054297L/no

Links

Classifications

    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07B—GENERAL METHODS OF ORGANIC CHEMISTRY; APPARATUS THEREFOR
    • C07B35/00—Reactions without formation or introduction of functional groups containing hetero atoms, involving a change in the type of bonding between two carbon atoms already directly linked
    • C07B35/04—Dehydrogenation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0446—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical
    • B01J8/0449—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds
    • B01J8/0453—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds the flow within the beds being predominantly vertical in two or more cylindrical beds the beds being superimposed one above the other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0492—Feeding reactive fluids
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J8/00—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes
    • B01J8/02—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds
    • B01J8/04—Chemical or physical processes in general, conducted in the presence of fluids and solid particles; Apparatus for such processes with stationary particles, e.g. in fixed beds the fluid passing successively through two or more beds
    • B01J8/0496—Heating or cooling the reactor
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C4/00—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms
    • C07C4/08—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule
    • C07C4/10—Preparation of hydrocarbons from hydrocarbons containing a larger number of carbon atoms by splitting-off an aliphatic or cycloaliphatic part from the molecule from acyclic hydrocarbons
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C5/00—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms
    • C07C5/42—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor
    • C07C5/48—Preparation of hydrocarbons from hydrocarbons containing the same number of carbon atoms by dehydrogenation with a hydrogen acceptor with oxygen as an acceptor
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2208/00—Processes carried out in the presence of solid particles; Reactors therefor
    • B01J2208/00008—Controlling the process
    • B01J2208/00017—Controlling the temperature
    • B01J2208/00522—Controlling the temperature using inert heat absorbing solids outside the bed
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00051—Controlling the temperature
    • B01J2219/00074—Controlling the temperature by indirect heating or cooling employing heat exchange fluids
    • B01J2219/00087—Controlling the temperature by indirect heating or cooling employing heat exchange fluids with heat exchange elements outside the reactor
    • B01J2219/00094—Jackets
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2219/00—Chemical, physical or physico-chemical processes in general; Their relevant apparatus
    • B01J2219/00049—Controlling or regulating processes
    • B01J2219/00245—Avoiding undesirable reactions or side-effects
    • B01J2219/00259—Preventing runaway of the chemical reaction
    • B01J2219/00265—Preventing flame propagation

Landscapes

  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
  • Devices And Processes Conducted In The Presence Of Fluids And Solid Particles (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
  • Fire-Extinguishing Compositions (AREA)

Abstract

Det tilveiebringes en reaktorkonstruksjon som muliggjør at en autotermisk krakkingsprosess kan gjennomføres ved et hvilket som helst egnet trykk der de gassformige reaktanter forvarmes separat før blanding og sa presenteres til reaksjonssonen på enhetlig fordelt måte. Særlig beskrives det en apparatur for omsetning av en første og en andre gassformig reaktant for å danne et gassformig produkt der apparaturen omfatter minst en første tilførselsinnretning for den første gassformige reaktant, minst en andre tilførselsinnretning for den andre gassformige reaktant, en motstandssone, og en reaksjonssone, fortrinnsvis omfattende en katalysator, der den første tilførselsinnretning omfatter et antall første utløp for avlevering av den første, gassformige reaktant, og den andre tilførselsinnretning omfatter et antall andre utløp for avlevering av den andre, gassformige reaktant, der videre motstandssonen er porøs, og der reaksjonssonen er posisjonert nedstrøms for motstandssonen i forhold til strømningsretningen for den første og andre gassformige reaktant, og der de første tilførselsinnretninger og andre tilførselsinnretninger er anordnet slik at den første gass og den andre gass kommer i kontakt på i det vesentlige parallell måte og blandes før kontakt med motstandssonen. Det beskrives videre en fremgangsmåte for fremstilling av et monoolefin ved bruk av denne apparatur.
NO20054297A 2003-02-18 2005-09-16 Automatisk krakkingsreaktor NO20054297L (no)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB0303723A GB0303723D0 (en) 2003-02-18 2003-02-18 Auto thermal cracking reactor
GB0329710A GB0329710D0 (en) 2003-12-22 2003-12-22 Autothermal cracking process
PCT/GB2004/000488 WO2004074222A1 (en) 2003-02-18 2004-02-06 Auto thermal cracking reactor

Publications (1)

Publication Number Publication Date
NO20054297L true NO20054297L (no) 2005-09-16

Family

ID=32910463

Family Applications (1)

Application Number Title Priority Date Filing Date
NO20054297A NO20054297L (no) 2003-02-18 2005-09-16 Automatisk krakkingsreaktor

Country Status (17)

Country Link
US (1) US7807860B2 (no)
EP (1) EP1594823B1 (no)
JP (1) JP5054375B2 (no)
KR (1) KR20050111327A (no)
AR (1) AR043192A1 (no)
AU (1) AU2004213211A1 (no)
BR (1) BRPI0407575A (no)
CA (1) CA2516247C (no)
EA (1) EA007370B1 (no)
HR (1) HRP20050811A2 (no)
MX (1) MXPA05008772A (no)
MY (1) MY133424A (no)
NO (1) NO20054297L (no)
PL (1) PL377262A1 (no)
RS (1) RS20050632A (no)
TW (1) TW200422289A (no)
WO (1) WO2004074222A1 (no)

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US7901662B2 (en) * 2005-11-01 2011-03-08 Celanese International Corporation Steam generation apparatus and method
WO2007071925A1 (en) * 2005-12-20 2007-06-28 Ineos Europe Limited Catalyst holder, apparatus containing it and process for the reaction of an hydrocarbon with oxygen
EP2004578B1 (de) 2006-03-30 2014-09-03 Basf Se Verfahren einer heterogen katalysierten partiellen dehydrierung wenigstens eines zu dehydrierenden kohlenwasserstoffs
US7842846B2 (en) 2006-03-30 2010-11-30 Basf Aktiengesellschaft Process for heterogeneously catalyzed partial dehydrogenation of at least one hydrocarbon to be dehydrogenated
RU2448080C2 (ru) * 2006-03-30 2012-04-20 Басф Се Способ гетерогенного каталитического парциального дегидрирования по меньшей мере одного подлежащего дегидрированию углеводорода
GB0613676D0 (en) 2006-07-10 2006-08-16 Ineos Europe Ltd Process
DE102006054415A1 (de) * 2006-11-16 2008-05-21 Uhde Gmbh Verfahren und Vorrichtung zum Eindüsen von Sauerstoff in ein einen Synthesereaktor durchströmendes Reaktionsgas
US8262755B2 (en) * 2007-06-05 2012-09-11 Air Products And Chemicals, Inc. Staged membrane oxidation reactor system
EP2045002A1 (en) 2007-10-02 2009-04-08 Ineos Europe Limited Mixing apparatus
EP2572776A1 (en) * 2011-09-21 2013-03-27 Evonik Degussa GmbH Device for mixing and cooling two reactive liquids and method of making peroxomonosulphuric acid with the device
EP2572781A1 (en) 2011-09-21 2013-03-27 Evonik Degussa GmbH Device and method for making a dilute aqueous solution of peroxomonosulphuric acid
CN102600787A (zh) * 2012-03-30 2012-07-25 凯莱英医药集团（天津）股份有限公司 臭氧化连续反应装置及其工作方法
RU2534991C1 (ru) * 2013-04-22 2014-12-10 Юрий Николаевич Филимонов Устройство для получения непредельных углеводородов, преимущественно этилена
CN111689861B (zh) * 2019-03-11 2022-04-12 北京诺维新材科技有限公司 一种提高反应收率的方法
CN113522192B (zh) * 2020-04-20 2022-10-21 中国石油化工股份有限公司 制备聚α-烯烃的装置和方法

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US3320331A (en) * 1966-01-27 1967-05-16 Exxon Research Engineering Co Oxidative dehydrogenation of aliphatic hydrocarbons over aluminum phosphate supported molybdenum and vanadium
SU255912A1 (ru) 1968-07-11 1983-05-15 Институт газа АН УССР Реактор термоокислительного пиролиза углеводородов
SU435633A1 (ru) 1970-08-10 1982-06-15 В. Ф. Попов Газораспределительное устройство
US3881701A (en) * 1973-09-17 1975-05-06 Aerojet General Co Fluid mixer reactor
US4865820A (en) * 1987-08-14 1989-09-12 Davy Mckee Corporation Gas mixer and distributor for reactor
GB8805447D0 (en) 1988-03-08 1988-04-07 British Petroleum Co Plc Chemical process
US5106590A (en) * 1990-05-11 1992-04-21 Davy Mckee (London) Limited Gas mixer and distributor with heat exchange between incoming gases
US5399307A (en) 1993-06-18 1995-03-21 Dalton; Robert E. Methods of compression molding two or more polytetrafluoroethylene resin layers
NO300117B1 (no) 1994-12-22 1997-04-14 Norske Stats Oljeselskap Reaktor for dehydrogenering av hydrokarboner med selektiv oksidasjon av hydrogen
US5905180A (en) 1996-01-22 1999-05-18 Regents Of The University Of Minnesota Catalytic oxidative dehydrogenation process and catalyst
US6267912B1 (en) 1997-04-25 2001-07-31 Exxon Research And Engineering Co. Distributed injection catalytic partial oxidation process and apparatus for producing synthesis gas
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EP1206316B1 (en) 1999-08-17 2005-06-29 Battelle Memorial Institute Chemical reactor and method for catalytic gas phase reactions
AU777051B2 (en) 1999-12-23 2004-09-30 Ineos Europe Limited Process for the production of olefins
CA2395376A1 (en) 1999-12-23 2001-07-05 Bp Chemicals Limited Process for the production of olefins
GB0010693D0 (en) * 2000-05-03 2000-06-28 Bp Chem Int Ltd Process for the production of olefins
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US7097787B2 (en) 2002-07-19 2006-08-29 Conocophillips Company Utilization of micro-channel gas distributor to distribute unreacted feed gas into reactors

Also Published As

Publication number Publication date
CA2516247C (en) 2013-05-28
MXPA05008772A (es) 2006-03-21
AU2004213211A8 (en) 2004-09-02
MY133424A (en) 2007-11-30
BRPI0407575A (pt) 2006-02-14
HRP20050811A2 (en) 2005-10-31
RS20050632A (en) 2007-12-31
EP1594823B1 (en) 2016-08-17
KR20050111327A (ko) 2005-11-24
EP1594823A1 (en) 2005-11-16
US20060149114A1 (en) 2006-07-06
JP5054375B2 (ja) 2012-10-24
US7807860B2 (en) 2010-10-05
AR043192A1 (es) 2005-07-20
AU2004213211A1 (en) 2004-09-02
EA200501225A1 (ru) 2006-04-28
CA2516247A1 (en) 2004-09-02
PL377262A1 (pl) 2006-01-23
TW200422289A (en) 2004-11-01
WO2004074222A1 (en) 2004-09-02
JP2006517956A (ja) 2006-08-03
EA007370B1 (ru) 2006-10-27

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